Method for blanching vegetable materials



April 10, 1945. A. E. wlcal-:LswoR-rl-i` I METHOD FOR BLANCHING VEGETABLE MATERIALS Filed NOV. 24, 1942 5 Sheets-Sheet l' Aem/11951 Weaswoehj.

1N VENTOR.

ATTORNEY.

April 1o, 1945.

A. E. WIGELSWORTH METHOD FOR BLANCHING YEGETABLE MATERIALS Filed Nov. 24, 1942 s sheets-sheet 2 NN o o o o A P o o o o o o o o o. o o o o o o o o o o o, .0. o o o @.J o o o o NN. o o o o o (o o o o o o o o. o o o 0..... o o o o o o o o o vo o o l@ o o o o o o. o o o o o -.o.... o vo o o o o w......, o o o o o .91.- 1 o o o o o 9. o o o o o o ,o a O 0 a o QM..

.0 o o o o o o INVENTOR.

y ATTORNEY.

April 10, 1945.

A; E. w| 3|5| swORTx-|- METHOD FOR BLANCHING' VEGETABLE MATERIALS Filed Nov. A24, 1942 :s sheets-sheet :sl

Aem/125i Mausi/VORM,

INVENTOR BY WM ATTORNEY.

blanching chamber and circulated over and past the material until the temperature thereof has been reduced suiiiciently to prevent occurrence of any undesired changes in the material and to permit handling thereof. The cool gas employed in this cooling step is preferably unsaturated with water vapor, as is the case when ordinary atmospheric air is introduced, and its capacity to pick up water vapor is increased as it becomes heated upon entering the apparatus. Consequently there is a considerable evaporation of water from the material during this stage, which contributes to the cooling effect and also causes a partial drying of the blanched material.

The method of vthe present invention may be carried out in an apparatus comprising a rectangular housing provided with door means at one end and adapted to receive a car or truck carrying a plurality'of trays on which the material to be blanched is spread out. The trays are arranged in the truck in such manner that a gaseous heating medium (steam) or a cooling medium (such as air) can be circulated over and under the material to be treated, transversely of the housing. At the respective sides of the housing, inlet and outlet manifold spaces are provided through which the gaseous medium may be introduced and withdrawn in such manner as to provide substantially uniform iiow thereof across the chamber, and a suitable circulating means such as a blower or the like is provided, together with connecting conduits, for maintaining a circulation of the medium within and through the housing. The apparatus is further provided with means for introducing a heating medium such as steam, preferably directly into the inlet manifold, to cause production of the desired conditions of temperature and humidity for blanching. Cooperating wth the circulatory system, the apparatus is further .preferably provided with a damper arrangement whereby the continued re` circulation of the gaseous medium may be interrupted and a cooling medium such as atmospheric air may be drawn into the housing, passed in contact with the blanched material, and subsequently discharged from the apparatus.

The above and other features will be brought out in the ensuing description of a preferred embodiment of the apparatus and of the preferred practice of the method, or will be apparent from such description. A preferred form of apparatus is illustrated in the accompanying drawings in which:

Fig. 1 is a partly broken away plan view of the apparatus;

Fig. 2 is a partly broken away sectional elevation of the apparatus as taken on line 2-2 in Fig. 1; and

Fig. 3 is a, transverse section thereof as taken on line 3-3 in Fig. 1.

Referring to the drawings, the device is shown as comprising a rectangular housing defined by side walls I and 2, an end wall 3, a top wal1'4 and a vertical slidable door member 5 dening'the opposite end wall. The side walls I and l2 are exteriorly insulated as at I a and 2a and are provided with interior wall members 6 and 1, respectively, spaced inwardly from the respective side walls I and 2 so as to define longitudinally and vertically extending spaces 8 and'9 which may comprise the inlet and outlet manifolds for the desired circulation of the heating and cooling medium. The space between the inner wall members 6 and 1 constitutes the blanching chamber. The walls 6 and 'I are provided with a plurality of perforations II through which the desired circulation of gaseous medium is caused to take place. Said perfor-ations II are distributed substantially uniformly over the portions of wall members 6 and I between which the material to be blanched is disposed as described hereinafter.

The upper wall 4 is provided with elongated slots or openings I2 and I3 above the respective inanifold spaces 8 and 9, and suitable headers Ill and I5 are provided above the respective openings.

The gas circulatory system may comprise a blower I6 having its inlet connected by duct Il t0 the outlet header I5 and its outlet connected by duct i8 to the inlet header I4. The duct I8 is provided with an inlet duct or opening I9, communicating With the atmosphere, and a discharge duct or stack 2I also communicating with the atmosphere or other point of discharge, together with a movably mounted damper member 22 adapted to be located in a position such as shown in full lines in Fig. 3 wherein the duct I8 is caused to be continuous and open to communication from the blower I6 to the header I4, and communication between duct I8 and both ducts I9 and 2| is shut off. The damper further is adapted to be moved to an alternative position such as is indicated in dot-dash lines at 22 in Fig. 3 wherein the duct I8 is divided into separate compartments Ia and 18h, the former of which is in communication with the stack 2 I while the space Ib is in communication with the inlet duct I9. A suitable operating lever 22a may be provided to move the damper 22 between the indicated positions. With the damper in the full line position the blower I6, operated through the agency of a motor or the like 23, is adapted to force the gaseous medium into the inlet manifold space 8 and withdraw the medium from the outlet manifold space 9, keeping the gaseous medium in constant circulation past the material to be blanched. The material to be blanched is located on a plurality of trays 24 (preferably screen-bottomed) mounted on a truck or car 25 which is disposed within the blanching chamber defined between the perforated wall members 6 and 1, the top wall 4, the end wall 3 and the door 5.

In order to secure the desired heating of the material on the trays 24 live steam is introduced to the inlet manifold space 8 as through the agency of a steam manifold 26 provided with an inlet line 21 .and a plurality of discharge nozzles 28. The inlet steam line 2T is provided with a main steam valve 41 and with a control valve 29 which may be associated with a thermostatic control mechanism indicated at 3| through conventional circuit means, not shown, whereby the admission of steam through the line 21 may be interrupted when the temperature, as measured at the exhaust duct I7, reaches the desired maximum value. A thermostatic control element such as vapor pressure temperature bulb may be 1ocated in the duct I'I as indicated at 32. The housing I is conveniently made of such size as to receive a pair of trucks or cars 25, but one of which is indicated in Fig. 2.

The apparatus may be employed in the blanching treatment of a particular material according to the method of this invention in the following manner: A pair of trucks 25, each loaded to the desired extent with a plurality of trays 24 on which the particular material is evenly spread, are placed within the apparatus. The door 5 is adapted for vertical movement within guide members 40 and is conveniently provided with a counterweight 4I carried by cables 42 passed over -face moisture.

. gereset por 'the like in -lwnieh rarein turn carried en fe Ksu'iintie .superstrueture 4l. iwi-ien the api paratus is charged with the two trucks, cuilatory system is :placed fi-n operation by tener- .giziingthe motor 23,' :drivtng the-'inlener 111i. `1li-'re' @laitierl N is "placed the .ruiiaiine position for Figi. 53,'fand the circulation li's `Tt-lius 1 establi'shfitl Eas va continuous ite-circulationthroughfthe duct` `iti and manifold 1s, through :the :perforationsr l l @in the plate :or walls, then-ee across the space occupied bythe itru'clrstlienoe tlirou'glhltheopenings 11| in 1the wail i into thelspace 9 .and back through 'duct '41 to the blower It.- Tnevalve means t] fris then opened to-aurnitsteam totnemanifeldspace" 1 8, mixing withland heating fthe cireulatedair byfdirect contactfand yrcndensationithereupon. e

The @recirculation for ne .gaseous inediuiniseturate-u' with water 'vapor Lisitcentinueu 'unitn the v desired temperature has been attained 'asimeas fby thel bulb 13'2, `fior example), whereupon theyalve L29 will be actuatedzthr'ough tneiageney ltrays 24.

The temperature and time of blanching vary somewhat with-different vegetable materials. In

general, thevtemperature should be maintained tion of further steam as the body of gaseous between 180 and 212 F., and in most cases a temperature between about 190 and 200 F. is satisfactory. The time required varies, for example, from about two or three minutes for some materials such as cabbage or celery, to about ten minutes for other materials such as carrots or turnips. For most vegetables, the time required is between these limits, although it will of course be understood that the invention is not limited to any particular time or temperature of treatment. y

When the desired blanching period has elapsed, as indicated by the timer 46, the vmain steam valve 41 in the steam line 21 may be closed, and the damper 22 moved to the dot-dash position shown in Fig. 3. More preferably, I may incorporate the timer 46 in the circuit of the valve 28so that when the desired time has elapsed the steam line is closedl at the valve 29, automatically. Contin` ued operation of the blower I6 will thus cause atmospheric air atv relatively low temperature to be drawn in through the opening I8 into the passage portion lb, through the space 8 into the blanching chamber, thence into the space Sand out to the atmosphere through the header l5, blower I6, duct I8, and stack 2|.

The circulation of atmospheric air through the `blanching chamber and in Contact with the heated material on the trays 24 will result in a prompt cooling of this material by direct heat transfer and by cooling Thus, part of the sensible heat of the material is utilized to effect a partial dehydration of the material following the blanching operation. The rapid and uniform reduction of the temperature provides a sharp control of the effects of the heat treatment and prevents undeproduced by evaporation of sur- .v

sire-densas um sometimes l'erreur if the snare.

naifor la portion er `vit showed to remain at' temperatures above demandera penedrmaterially longer than eis ietually required ifor lf'e'e'e'titfe blanching. When the temperature of thefmateri'al :haslbeenreducedftora reasonably; low value,

such as 'in the .neighborhood fof .120 F., the 'doorv 5 may -rbe raised rand vthe .25 Withdrawn. This allowable .low temperature `may :be `indicated by the ibulbffS, if `desired. 'The apparatus 'is thus :ready for to. repetition fof `the blanching 'cycle bnranewset-cfloadedtrucks.

Whil'evl shaveshown the "damper 2f2 .as 'being manuallyrcontrolled, it will 'be 'apparent to fthose skilled in the Sart that automatic Aoperation of this dampermasa :result Aof completion y-of the blanching cycle may .readily be provided. :Similarlygothermodications of the construction will occur toi-those `skil.led:iln the @truand-for this reason -I do `not choose to be .limited to the specific details of construction herein described, :but rather to :the scope of thesubjoinedeclaims vAccording -to .the method .wherein described, the material to-"be rblahched issubjected to substantially-.uniform ,contact a body of gaseous medium `containing livesteam. supplied through the-heaxierand iets-28. Thislive-steamfisinot permitted to directly impinge upon the mate-- rial on the trays 24 but rather is caused to be disseminated through the manifoldl space 8 and to be drawn past the material on the trays 24 through the openings' I I, as an evenly distributed uniformly heated and substantially saturated mass which generally also contains some condensed water particles ,carried in suspension.` This gaseous heating agent consists principally of air atthe start of the blanching procedure, and the proportion of steam is increased by the addimedium, is recrculated. The gaseous heating agent (mixed gasand steam) is thus introduced vsubstantially uniformly over one entire side of of such zone 'and consequent uniform heating of all parts o-f the material on the trays. As the body of gaseous medium is further saturated by additional steam and the temperature thereof in.. .creases .to-ward the temperature of the inlet steam, as a maximum, the temperature of the material on the trays 24 also increases, so that no great temperature differential between the material and the gaseous mediuniis ever lencountered. For this reason the material undergoing treatment is caused to be brought upto temperature in a very uniform fashion, and overblanching of portions of the material is to all purposes completely eliminated. Similarly, when the blanching treatment has been continued for the desired lengthr of time the immediate introduction and uniform circulation of atmospheric air will start to cool the material down to the desired handling .temperature with `substantially the same degree of uniformity vas was attained during the heating step. It has been observed that the constant introduction of the heated gaseous mixture throughout substantially the full height and length of the chamber, as from the space 8, andthe :comparable withdrawal of the mixture throughout substantially the entire height and length o-f the chamber, as through the space 9, maintains a very even temperature throughout the chamber as a whole and elimi-4 nates any dead air spaces or uneven distribution ofsteam and consequent heating which would interfere with even blanching of the material.. y

I claim: Y

1. The method of blanching vegetable Imaterial which comprises placing such material in a blanching zone Within an enclosed chamber; passing a gaseous medium substantially uniformly across said zone and in contact with the material therein, and recirculating the gaseous medium in a path including said zone; introducing live steam into the recirculated gaseous medium at a position removed from the blanchingzone until the gaseous medium is heated to blanching temperature and is substantially saturated with water vapor; and continuing such recirculation to subject the material to direct contact with the resulting heated and substantially saturated gaseous medium until the .desired blanching treatment is effected.

2i. The method as set forth in claim l and including .the subsequent steps of discontinuing such recirculation when the blanching treatment is completed, and thereupon introducing a relatively cool vgaseous medium into said zone and discharging it therefrom after Contact with said material, to quickly reduce the temperature of the material and cause evaporation of water therefrom.

3. The method of blanching vegetable material which comprises: placing the material in dis tributed condition at a plurality of levels in a substantially enclosed chamber; introducing a bodyI of gaseous medium. at one side of the chamber substantially uniformly over such side and similarly withdrawing such body from the opposite side of such chamber; maintaining such body in continuo-us recirculation through said chamber; introducing live steam into admixture with said body at a position exteriorly of said chamber whereby .the temperature of said body is increased to the desired blanching temperature; maintaining recirculation of said body together with steam so introduced, until the desired blanching treatment has been eiected; and thereupon introducing a relatively cool body of gaseous medium to said chamber in the absence of added live steam, and discharging such body from. said chamber after contact with the material therein, until the temperature of said material is reduced suiciently for handling.

ARTHUR E. W'IGELSWORTH. 

